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the coking properties of coal at elevated pressures. - Argonne ...

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under which conditions sulfur species gener<strong>at</strong>ed during <strong>the</strong> combustion <strong>of</strong> pulverized<br />

<strong>coal</strong> can be captured and retained by calcium containing sorbents. Two series <strong>of</strong><br />

experiments were carried out: one in which any capture would take place primarily<br />

under oxidizing conditions and <strong>the</strong> o<strong>the</strong>r in which significant residence times in<br />

<strong>the</strong> rich zone would allow capture under reducing conditions. Under oxidizing conditions<br />

<strong>the</strong> <strong>the</strong>rmal environment experienced by <strong>the</strong> sorbent particle appears to be <strong>the</strong><br />

dominant parameter controlling sulfur capture. This is probably because <strong>of</strong> deadburning.<br />

If a sorbent particle's temper<strong>at</strong>ure exceeds a certain limit (which depends<br />

on <strong>the</strong> particular sorbent) <strong>the</strong> sorbent deadburns and loses its reactivity (4).<br />

The processes controlling capture and retention when <strong>the</strong> sorbent is maintained<br />

under reducing conditions for a prolonged time are more complex. The principle<br />

gas phase sulfur specie are HzS, SO2 and COS and, even though <strong>the</strong> sulfur species are<br />

absorbed <strong>the</strong> possibility th<strong>at</strong> <strong>the</strong> sulfide will decompose during burnout exists.<br />

The d<strong>at</strong>a presented in Figure 6 shows a significant difference between <strong>the</strong> behavior<br />

<strong>of</strong> <strong>coal</strong> and propane doped with H2S. This difference can be <strong>at</strong>tributed to:<br />

- With <strong>coal</strong> part <strong>of</strong> <strong>the</strong> fuel remains in <strong>the</strong> solid phase and for a given<br />

input stoichiometry <strong>the</strong> gas phase stoichiometry in <strong>the</strong> reducing zone is<br />

higher than with gas. Reference to Figure 1 indic<strong>at</strong>es th<strong>at</strong> <strong>the</strong> stability<br />

<strong>of</strong> calcium sulfide is strongly dependent upon stoichiometry r<strong>at</strong>io;<br />

-<br />

With <strong>coal</strong> up to 50 percent <strong>of</strong> <strong>the</strong> sulfur remains in <strong>the</strong> solid phase under<br />

rich conditions thus <strong>the</strong> gas phase concentr<strong>at</strong>ion is lower than <strong>the</strong> corres-<br />

ponding concentr<strong>at</strong>ion with propane as <strong>the</strong> fuel;<br />

- The conditions during burnout in <strong>the</strong> second stage will be different for <strong>the</strong><br />

solid and gaseous fuels and this could affect retention <strong>of</strong> <strong>the</strong> sulfur<br />

during burnout.<br />

These tests indic<strong>at</strong>e th<strong>at</strong> <strong>the</strong>re is <strong>the</strong> potential to remove gre<strong>at</strong>er than 50<br />

percent <strong>of</strong> <strong>the</strong> input sulfur with Ca/S molar r<strong>at</strong>ios <strong>of</strong> two when <strong>coal</strong> is burned<br />

under low NOx conditions. Fur<strong>the</strong>r work is necessary to insure th<strong>at</strong> <strong>the</strong> controlling<br />

conditions can be achieved in practical combustors and th<strong>at</strong> <strong>the</strong> sorbent injection<br />

does not adversely impact combustor performance.<br />

References<br />

1.<br />

2.<br />

3.<br />

4.<br />

5.<br />

6.<br />

Gartrell, F.F., "Full Scale Desulfuriz<strong>at</strong>ion <strong>of</strong> Stack Gas by Dry Limestone<br />

Injection", EPA-650/2-73-019 a, b, c, 1973.<br />

Zallen, D.M., Gershman, R., Heap, M.P., Nurick, W.H., "The Generaliz<strong>at</strong>ion <strong>of</strong><br />

Low Emission Coal Burner Technology", Proceedings, Third St<strong>at</strong>ionary Source<br />

Combustion Symposium, EPA-600/7-70-050 b, 1979.<br />

Flament, G., "The Simultaneous Reduction <strong>of</strong> NOx and SO2 in Coal Flames by<br />

Direct Injection <strong>of</strong> Sorbents in a Staged Mixing Burner", IFRF doc. no.<br />

G 19/a/10, 1981.<br />

Coutant, R.W., et al., "Investig<strong>at</strong>ion <strong>of</strong> <strong>the</strong> Reactivity <strong>of</strong> Limestone and<br />

Dolomite for Capturing SO2 from Flue Gas", B<strong>at</strong>elle Memorial Institute,<br />

Final Report, EPA Contract PH-86-67-115, 1970.<br />

Borgwardt, R.H., "Kinetic <strong>of</strong> <strong>the</strong> Reaction <strong>of</strong> SO2 with Calcined Limestone",<br />

NAPCA, Vol. 4, p. 59, 1970.<br />

Borgwardt, R.H., Present<strong>at</strong>ion <strong>at</strong> <strong>the</strong> EPA SPO Contractors Meeting, Raleigh,<br />

North Carolina, October 1981.<br />

165

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